The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Sep. 14, 2021

Filed:

Aug. 20, 2020
Applicant:

Exxonmobil Chemical Patents Inc., Baytown, TX (US);

Inventors:

Keith W. Trapp, Kingwood, TX (US);

Scott T. Roger, Porter, TX (US);

James A. Kendrick, Greenwell Springs, LA (US);

Edward F. Smith, Doylestown, PA (US);

Assignee:
Attorney:
Primary Examiner:
Int. Cl.
CPC ...
C08F 2/01 (2006.01); B01D 5/00 (2006.01); B01J 8/00 (2006.01); B01J 19/24 (2006.01); C08F 2/06 (2006.01); C08F 6/02 (2006.01); C08F 6/10 (2006.01); C08F 110/02 (2006.01); C08F 210/16 (2006.01);
U.S. Cl.
CPC ...
C08F 2/01 (2013.01); B01D 5/0003 (2013.01); B01J 8/005 (2013.01); B01J 8/0015 (2013.01); B01J 19/242 (2013.01); C08F 2/06 (2013.01); C08F 6/02 (2013.01); C08F 6/10 (2013.01); C08F 110/02 (2013.01); C08F 210/16 (2013.01); B01J 2219/0004 (2013.01); B01J 2219/00042 (2013.01);
Abstract

Processes and apparatus for preparing bimodal polymers are provided. In some embodiments, processes include introducing a monomer, a first diluent, a catalyst, hydrogen, at a first hydrogen concentration, and optional comonomer, to a first loop reactor to produce, under polymerization conditions, a first slurry of polymer solids. Processes may also include continuously discharging the first slurry of polymer solids from the loop reactor as a first polymerization effluent to a first flash tank; separating the first polymerization effluent in the first flash tank to provide a first concentrated polymer slurry with significantly lower hydrogen concentration; and transferring the first concentrated polymer slurry from the flash tank to a re-slurry mixer. Processes may further include introducing a re-slurry mixer diluent to the first concentrated polymer slurry to form a second concentrated polymer slurry in the re-slurry mixer that can be pumped to a second slurry loop reactor.


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